US4992523A - Copolymers containing si-n and si-si bonds, polycarbosilazanes obtained by pyrolysis of the said copolymers, and use of the said polycarbosilazanes for the preparation of silicon carbonitride - Google Patents

Copolymers containing si-n and si-si bonds, polycarbosilazanes obtained by pyrolysis of the said copolymers, and use of the said polycarbosilazanes for the preparation of silicon carbonitride Download PDF

Info

Publication number
US4992523A
US4992523A US07/204,677 US20467788A US4992523A US 4992523 A US4992523 A US 4992523A US 20467788 A US20467788 A US 20467788A US 4992523 A US4992523 A US 4992523A
Authority
US
United States
Prior art keywords
mol
copolymers
polycarbosilazanes
copolymer
soluble
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
US07/204,677
Inventor
Eric Bacque
Jean-Paul Pillot
Jacques Dunogues
Pierre Olry
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EUROPEENNE DE PROPULSION - A FRENCH Corp DULY ORGANIZED UNDER LAWS OF FRANCE SA Ste
Rhodia Chimie SAS
Original Assignee
Societe Europeenne de Propulsion SEP SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Societe Europeenne de Propulsion SEP SA filed Critical Societe Europeenne de Propulsion SEP SA
Assigned to SOCIETE ANONYME: SOCIETE EUROPEENNE DE PROPULSION - A FRENCH CORPORATION DULY ORGANIZED UNDER THE LAWS OF FRANCE reassignment SOCIETE ANONYME: SOCIETE EUROPEENNE DE PROPULSION - A FRENCH CORPORATION DULY ORGANIZED UNDER THE LAWS OF FRANCE ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: BACQUE, ERIC, DUNOGUES, JACQUES, OLRY, PIERRE, PILLOT, JEAN-PAUL
Assigned to RHONE-POULENC CHIMIE reassignment RHONE-POULENC CHIMIE ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: SOCIETE ANONYME: SOCIETE EUROPEENNE DE PROPULSION
Application granted granted Critical
Publication of US4992523A publication Critical patent/US4992523A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/60Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule in which all the silicon atoms are connected by linkages other than oxygen atoms
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
    • C04B35/56Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides
    • C04B35/565Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides based on silicon carbide
    • C04B35/571Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides based on silicon carbide obtained from Si-containing polymer precursors or organosilicon monomers
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
    • C04B35/58Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides
    • C04B35/584Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on silicon nitride
    • C04B35/589Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on silicon nitride obtained from Si-containing polymer precursors or organosilicon monomers

Definitions

  • the present invention relates to copolymers containing --Si--N-- and --Si--Si-- bonds, which are obtained by the polycondensation of
  • R 2 Is a halogen atom, preferably Br and Cl, and
  • R, R 1 and R 3 which are identical or different, represent a hydrogen atom or an alkyl, alkenyl, alkynyl, cycloalkyl, cycloalkenyl, aryl, alkylaryl or alkenylaryl hydrocarbon radical which may be functional.
  • the copolymers according to the invention contain, in their main chain, --Si--Si--Si-- sequences originating from monomer (B), --Si--Si-- n sequences, where n ⁇ 1, originating from monomer (A), and --Si--(Si) n --Si--N-- sequences, where n ⁇ 1, originating from the linking of both monomers.
  • the copolymer obtained contains an Si--H bond, which makes it possible subsequently to carry out chemical or thermal cross-linking reactions on the product.
  • chlorinated disilane of the formula Cl x SiMe 3-x --SiMe 3-y Cl y in which 1 ⁇ x ⁇ 3 and 1 ⁇ y ⁇ 3, may be used as the silane Mixtures of chlorinated disilanes, such as those recovered in the industrial synthesis of chlorosilanes, may also be used.
  • polysilane-polysilazanes claimed in the present invention are the possibility afforded by these products of effecting the thermal conversion of ##STR3## linkages to ##STR4## linkages (c.f., for example, S. JAMIMA, Ceram. Bull. 1983, 62, 893 and references cited therein).
  • the polycarbosilazanes obtained are not only novel but can also be obtained in forms which are soluble, fusible without degradation under an inert atmosphere, spinnable, crosslinkable and with Si/C/N ratios which can vary within very wide limits.
  • These novel polycarbosilazanes are obtained by thermolysis of the copolymers at temperatures between 250° and 500° C. under an inert atmosphere; these polycarbosilazanes are excellent precursors for the production of matrices and fibers of silicon carbonitride, this silicon carbonitride being obtained by heating the polycarbosilazanes to temperatures of about 900°-1000° C. If these polycarbosilazanes have been produced according to the invention under a dry inert atmosphere, they contain no oxygen (or very little) provided a non-oxygenated solvent has been used in the copolymer formation step.
  • the process for the preparation of the copolymers according to the invention consists in bringing the comonomers together in chosen proportions in a solvent medium, in the presence of an alkali metal, more particularly sodium.
  • the solvent (or solvent mixture) which can be used may be toluene, xylene, a high-molecular alkane, a mixture of toluene and tetrahydrofuran, etc.
  • the copolymerization temperature is advantageously the boiling point of the solvent at atmospheric pressure.
  • the dimethyldichlorosilane was distilled before being used.
  • the toluene was dried by azeotropic distillation and the THF was treated with sodium in the presence of benzophenone in order to remove traces of water and peroxides.
  • the equipment used to perform the reaction consists of a 500 ml round-bottomed flask provided with a magnetic stirrer, a pressure-equalized dropping funnel, an inlet for inert gas (argon or nitrogen) and a decalin-cooled reflux condenser connected to a drying column (CaCl 2 ).
  • the solvent mixture consisting of 21.75 g of THF and 152 29 g of toluene, i.e. a total of 200 ml in a ratio of 1/7 by weight, is introduced first, followed by 29 g of sodium (1.26 g atoms, 5% excess).
  • the solvent mixture is heated to the reflux temperature and the sodium is granulated by vigorous stirring.
  • the mixture of dimethyldichlorosilane (65.82%, 0.51 mol) and (HMeClSi) 2 NH (15.67 g, 0.09 mol --15 mol %) is added dropwise.
  • the copolymer is soluble in solvents such as benzene, toluene, cyclohexane, heptane, carbon tetrachloride, ether, tetrahydrofuran etc.
  • Example 2 The experiment is carried out as in Example 1 with 200 ml of toluene, and no THF, as the solvent This gives 0.53 g of low-molecular products, 28 1 g of soluble copolymer (yield: 72.1%) and 6.6 g of insoluble solid copolymer.
  • Example 2 The experiment is carried out as in Example 1 with 175 ml of a toluene/THF mixture as the solvent (in the respective proportions of 7 to 1 by weight), 23 g of sodium (1 g atom), 41.1 g of Me 2 SiCl 2 (0.318 mol) and 18.5 g of (HClMeSi) 2 NH (0.106 mol, 25 mol %).
  • Example 2 The experiment is carried out as in Example 2 with 200 ml of toluene as the solvent, 25 g of sodium, 50.33 g of Me 2 SiCl 2 (0.39 mol) and 22.64 g of freshly distilled (HMeClSi) 2 NH (0.13 mol, 25 mol %). This gives 0.95 g of low-molecular products, 29.2 g of soluble copolymer (yield: 81.1%) and 2.15 g of insoluble solid.
  • Example 2 The experiment is carried out as in Example 2 with 250 ml of toluene as the solvent, 28.73 g of sodium (1.25 g atoms), 50.33 g of Me 2 SiCl 2 (0.39 mol) and 36.6 g of (HMeClSi) 2 NH (0.21 mol, 35 mol %). This gives 1.05 g of low-molecular products, 40.52 g of soluble copolymer (yield 91.3%) (viscous oil) and 0.95 g of insoluble copolymer
  • Example 2 The experiment is carried out as in Example 2 with 150 ml of toluene, 19.55 g of sodium (0.85 g atom), 25.81 g of Me 2 SiCl 2 (0.2 mol) and 34.83 g of (HMeSiCl) 2 NH (0.2 mol, 50 mol %). This gives 0.15 g of low-molecular products, 25.55 g of copolymer (soluble fluid oil) (yield: 79.2%) and 0.35 g of insoluble material.
  • Example 2 The experiment is carried out as in Example 2 with 125 ml of toluene, 19.3 g of sodium (0.84 g atom, 5% excess), 34.5 g of methyldichlorosilane (0.3 mol) and 17.4 g of (ClMeHSi) 2 NH (0.1 mol, 25 mol %). This gives 0.32 g of low-molecular products, 21.8 g of soluble copolymer (oil) (yield: 82.7%) and 1.5 g of insoluble copolymer.
  • Example 2 The experiment is carried out as in Example 1 with 300 ml of a toluene/THF mixture in the respective proportions of 7 to 1 by weight, 32.2 g of sodium (1.4 g atoms), 79.94 g of freshly distilled dichloromethylvinylsilane (0.566 mol) and 17.42 g of (HMeClSi) 2 NH (0.1 mol, 15 mol %). This gives 12.77 g of soluble copolymer (solid) (yield: 23%) and 41.4 g of insoluble solid copolymer (yield: 77%).
  • Example 2 The experiment is carried out as in Example 2 with 250 ml of toluene, 23 g of sodium (1 g atom), 50.78 g of dichloromethylvinylsilane (0.36 mol) and 20.9 g of (HMeClSi) 2 NH (0.12 mol, 25 mol %). This gives 17.95 g of soluble solid copolymer (yield: 43.4%) and 23.4 g of insoluble copolymer (56.6%).
  • Example 2 The experiment is carried out as in Example 2 with 200 ml of toluene, 25.3 g of sodium (1.1 g atoms), 43.62 g of Me 2 SiCl 2 (0.338 mol, 65 mol %), 7.33 g of dichloromethylvinylsilane (0.052 mol, 10 mol %) and 22.64 g of (HMeClSi) 2 NH (0.13 mol, 25 mol %).
  • Example 2 The experiment is carried out as in Example 1 with 300 ml of toluene as the solvent, 21 g of sodium (0.91 g atom), 61.7 g of chlorinated disilanes of the empirical formula Me 2 .3 Si 2 Cl 3 .7 and 26.1 g of (HMeClSi) 2 NH (0 15 mol, 35 mol %). This gives 10.5 g of soluble copolymer (yield: 25.78%) and 23.3 g of insoluble copolymer (yield: 69.71%).
  • Example 2 The experiment is carried out as in Example 2 with 125 ml of toluene, 16.1 g of sodium (0.7 g atom), 36.5 g of Me 2 SiCl 2 (0.28 mol) and 9.41 g of (HMeClSi) 2 NMe (0.05 mol, 15 mol %). This gives 2.14 g of low-molecular products, 17.5 g of soluble copolymer (yield: 80.8%) and 3.27 g of insoluble solid.
  • Example 2 The experiment is carried out as in Example 2 with 125 ml of toluene, 16.1 g of sodium (0.7 g atom), 36.5 g of Me 2 SiCl 2 (0.28 mol) and 10.1 g of (EtHClSi) 2 NH (0.05 mol, 15 mol %). This gives 1.07 g of low-molecular products, 16.98 g of soluble white grease (yield: 73.95%) and 2.62 g of insoluble solid.
  • Example 2 The experiment is carried out as in Example 2 with 120 ml of toluene, 13.5 g of sodium (0.59 g atom), 27.1 g of Me 2 SiCl 2 (0.21 mol) and 20.9 g of (HPhClSi) 2 NH (0.07 mol, 25 mol %). This gives 0.47 g of low-molecular products, 25.12 g of soluble copolymer (yield 89 3%) and 1.93 g of insoluble materials.
  • Example 2 The experiment is carried out as in Example 2 with 150 ml of toluene, 14.94 g of sodium (0.65 g atom), 48.74 g of PhMeSiCl 2 (0.255 mol) and 7.84 g of (HMeClSi) 2 NH (0.045 mol, 15 mol %). This gives 0.09 g of low-molecular products, 34.54 g of soluble copolymer (yield: 99.3%) and 0.15 g of insoluble solid.
  • Example 2 The experiment is carried out as in Example 2 with 160 ml of toluene, 16.1 g of sodium (0.7 g atom), 45.87 g of PhMeSiCl 2 (0.24 mol) and 13.93 g of (HMeClSi) 2 NH (0.08 mol, 25 mol %). This gives 0.23 g of low-molecular products, 36.64 g of soluble copolymer and 0.13 g of insoluble materials.
  • Example 2 The experiment is carried out as in Example 2 with 165 ml of toluene, 17.24 g of sodium (0.75 g atom), 37.3 g of Me 2 SiCl 2 (0.289 mol) and 10.11 g of (HViClSi) 2 NH (0.051 mol, 15 mol %). This gives 0.46 g of low-molecular products, 7.06 g of soluble grease (yield: 30.3%) and 18.27 g of insoluble materials.
  • the equipment consists of a 500 ml long-necked silica round-bottomed flask provided with a thermometer sleeve, an inlet for inert gas (argon) and a water-cooled silica reflux condenser connected to a precision gas meter.
  • the soluble copolymer prepared according to Example 1 is introduced into the flask under an inert atmosphere (13.95 g), it being possible for the material to be weighed in a glove box, and the equipment is then purged carefully with argon.
  • Thermolysis is effected by progressively heating the flask to a temperature of 500° C. by means of a fluidized sand bath. The operation is stopped after 5 h, at which point the temperature of the reactIon medIum has reached 433° C. and the total volume of gas evolved is 1725 cm 3 .
  • the volume of gas is 104.6 cm 3 /g, based on the mass of product used.
  • the contents of the flask are taken up with 200 cm 3 of hexane, after cooling, and stirred for one hour with a magnetic stirrer until optimum dissolution has been achieved.
  • Example 18 The experiment is carried out as in Example 18 using the copolymer prepared in Example 1 (13.95 g). Duration: 5 h. Temperature of the sand bath: 500° C. Final temperature of the reaction medium 413° C. Volume of gas (calculated as previously): 82.4 cm 3 /g.
  • Soluble polycarbosilazane 5.4 g (yield: 38.7%); Softening point: 190° C.; proportion of residue at 900° C.: 66%;
  • Insoluble polycarbosilazane 2.45 g
  • Example 18 The experiment is carried out as described in Example 18 using 12.8 g of copolymer prepared according to Example 2. Duration: 3 h 45 min. Temperature of the sand bath: 450° C. Final temperature of the reaction medium: 402° C. ##EQU1##
  • Soluble polycarbosilazane 6.7 g (yield: 52.3%); N (%): 3.72; Cl (%): 0.38; Softening point on Koffler bench 250° C.; Proportion of residue: 66% at 1400° C.;
  • Example 18 The experiment is carried out as described in Example 18 starting with 12.8 g of copolymer prepared according to Example 2. Duration: 4 h 30 min. Temperature of the sand bath: 425° C. Final temperature of the reaction medium: 390° C. ##EQU2##
  • Soluble polycarbosilazane 7.5 g (yield: 58.6%); N (%): 5.36; Cl (%): 0.50; Softening point on Koffler bench: 170° C.;
  • Soluble polycarbosilazane 4.2 g (yield: 36.7%); N (%): 3.88; Cl (%): 0.28; Softening point: 20° C.;
  • Soluble polycarbosilazane 4.35 g (yield: 36.5%); N (%): 3.37; Cl (%): ⁇ 0.01; Softening point: 50° C.;
  • Soluble polycarbosilazane 7.9 g (yield: 57.2%); Softening point: above 250° C.;
  • Soluble polycarbosilazane 9.3 g (yield 66.7%); N (%): 4.62; Cl (%): 0.7; Softening point: 110° C.;
  • Example 18 The experiment is carried out as described in Example 18 with 15 g of copolymer prepared according to Example 5. Duration of thermolysis: 4 h 30 min. Temperature of the sand bath: 400° C. Final temperature of the reaction medium 375° C. ##EQU7##
  • Soluble polycarbosilazane 10.2 g (yield: 68%); Softening point: 135° C.;
  • Example 18 The experiment is carried out as described in Example 18 starting with 15 g of copolymer prepared according to Example 5. DuratIon of thermolysis: 3 h min. Temperature of the sand bath: 400° C. Final temperature of the reaction medium: 373° C. ##EQU8##
  • Soluble polycarbosilazane 10 g (yield: 66.7%); Softening point: above 250° C.;
  • Example 18 The experiment is carried out as described in Example 18 starting with 11 g of copolymer prepared according to Example 7. Duration of thermolysis: 5 h. Temperature of the sand bath: 350° C. Final temperature of the reaction medium: 328° C. ##EQU9##

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Silicon Polymers (AREA)

Abstract

The present invention relates to copolymers containing --Si--N-- and --Si--Si-- bonds, which are obtained by the polycondensation of
at least one silane of the formula RR1 SiCl2
and at least one disilazane of the formula ##STR1## in which formulae: R2 is a halogen atom, preferably Br and Cl, and
R, R1 and R3, which are identical or different, represent a hydrogen atom or an alkyl, alkenyl, alkynyl, cycloalkyl, cycloalkenyl, aryl, alkylaryl or alkenylaryl hydrocarbon radical which may be functional,
to a process for the preparation of the said copolymers,
to the polycarbosilazanes obtained by thermolysis of the said copolymers and to the silicon carbonitrides obtained by heating the said polycarbosilazanes.

Description

The present invention relates to copolymers containing --Si--N-- and --Si--Si-- bonds, which are obtained by the polycondensation of
at least one silane of the formula
RR.sub.1 SiCl.sub.2                                        (A)
and at least one disilazane of the formula ##STR2## on which formulae: R2 Is a halogen atom, preferably Br and Cl, and
R, R1 and R3, which are identical or different, represent a hydrogen atom or an alkyl, alkenyl, alkynyl, cycloalkyl, cycloalkenyl, aryl, alkylaryl or alkenylaryl hydrocarbon radical which may be functional.
The proportions of A and B in the copolymer are unrestricted.
The copolymers according to the invention contain, in their main chain, --Si--Si--Si-- sequences originating from monomer (B), --Si--Si--n sequences, where n≧1, originating from monomer (A), and --Si--(Si)n --Si--N-- sequences, where n≧1, originating from the linking of both monomers.
It will be noted that, when at least one of the radicals R, R1 and R3 is hydrogen, the copolymer obtained contains an Si--H bond, which makes it possible subsequently to carry out chemical or thermal cross-linking reactions on the product.
Among the most valuable copolymers, there may be mentioned the products in which R2 =Cl, R1 =R3 =CH3 and R=H; these products form a particularly important sub-family because, to prepare the said copolymers, it is necessary to use only [(CH3)3 Cl--Si]2 NH, CH3 HSiCl2 and (CH3)2 SiCl2, which are commercial products and basic products for the synthesis of silicones.
Thus a chlorinated disilane of the formula Clx SiMe3-x --SiMe3-y Cly, in which 1<x<3 and 1<y<3, may be used as the silane Mixtures of chlorinated disilanes, such as those recovered in the industrial synthesis of chlorosilanes, may also be used.
One property of the polysilane-polysilazanes claimed in the present invention is the possibility afforded by these products of effecting the thermal conversion of ##STR3## linkages to ##STR4## linkages (c.f., for example, S. JAMIMA, Ceram. Bull. 1983, 62, 893 and references cited therein). The polycarbosilazanes obtained are not only novel but can also be obtained in forms which are soluble, fusible without degradation under an inert atmosphere, spinnable, crosslinkable and with Si/C/N ratios which can vary within very wide limits.
These novel polycarbosilazanes are obtained by thermolysis of the copolymers at temperatures between 250° and 500° C. under an inert atmosphere; these polycarbosilazanes are excellent precursors for the production of matrices and fibers of silicon carbonitride, this silicon carbonitride being obtained by heating the polycarbosilazanes to temperatures of about 900°-1000° C. If these polycarbosilazanes have been produced according to the invention under a dry inert atmosphere, they contain no oxygen (or very little) provided a non-oxygenated solvent has been used in the copolymer formation step.
The process for the preparation of the copolymers according to the invention consists in bringing the comonomers together in chosen proportions in a solvent medium, in the presence of an alkali metal, more particularly sodium. The solvent (or solvent mixture) which can be used may be toluene, xylene, a high-molecular alkane, a mixture of toluene and tetrahydrofuran, etc.
The copolymerization temperature is advantageously the boiling point of the solvent at atmospheric pressure.
The following Examples illustrate the invention:
EXAMPLE 1
In this Example as well as in those to follow, the dimethyldichlorosilane was distilled before being used. Likewise, the toluene was dried by azeotropic distillation and the THF was treated with sodium in the presence of benzophenone in order to remove traces of water and peroxides.
The equipment used to perform the reaction consists of a 500 ml round-bottomed flask provided with a magnetic stirrer, a pressure-equalized dropping funnel, an inlet for inert gas (argon or nitrogen) and a decalin-cooled reflux condenser connected to a drying column (CaCl2). The solvent mixture, consisting of 21.75 g of THF and 152 29 g of toluene, i.e. a total of 200 ml in a ratio of 1/7 by weight, is introduced first, followed by 29 g of sodium (1.26 g atoms, 5% excess).
The solvent mixture is heated to the reflux temperature and the sodium is granulated by vigorous stirring. When the dispersion of molten sodium is sufficiently fine, the mixture of dimethyldichlorosilane (65.82%, 0.51 mol) and (HMeClSi)2 NH (15.67 g, 0.09 mol --15 mol %) is added dropwise.
lt should be noted that, when the two chlorosilanes are mixed, a white turbidity appears which is probably due to a small amount of ammonium chloride
As soon as the first few drops are added, the medium becomes turbid and pale blue. A deep blue color appears within a few minutes. Addition time: 2 h. After 24 h under reflux, the mixture is allowed to cool under an inert atmosphere and is filtered on a frit, in a glove box, under an inert atmosphere. This gives a clear colorless solution. The blue solid remaining is taken up with toluene and the mixture is then filtered, this operation being performed twice. The two filtrates obtained in this way are combined with the first and the whole is concentrated under reduced pressure to give a grayish-blue fluid grease; this is then devolatilized under 1 mm of mercury, at 100° C. for 90 min, with the aid of a short distillation column equipped with a rectifier.
After cooling, the product has the appearance of an opaque, grayish-blue solidified grease Weight obtained: 32.9 g (yield: 84.6%). The copolymer is soluble in solvents such as benzene, toluene, cyclohexane, heptane, carbon tetrachloride, ether, tetrahydrofuran etc.
It is characterized by physicochemical methods (IR, NMR) and ty GC. The blue solid is further subjected to methanolysis and then hydrolysis, yielding a white pasty solid. After washing with solvents (acetone, ether), the solid is dried under vacuum (1 mm Hg) overnight at 140° C. to give 5.1 g of insoluble solid.
EXAMPLE 2
The experiment is carried out as in Example 1 with 200 ml of toluene, and no THF, as the solvent This gives 0.53 g of low-molecular products, 28 1 g of soluble copolymer (yield: 72.1%) and 6.6 g of insoluble solid copolymer.
EXAMPLE 3
The experiment is carried out as in Example 1 with 175 ml of a toluene/THF mixture as the solvent (in the respective proportions of 7 to 1 by weight), 23 g of sodium (1 g atom), 41.1 g of Me2 SiCl2 (0.318 mol) and 18.5 g of (HClMeSi)2 NH (0.106 mol, 25 mol %). This gives 1.45 g of low-molecular products, 25.45 g of soluble copolymer in the form of a grease which becomes fluid at 100° C. (yield: 86.4%), and 1.4 g of insoluble solid copolymer.
EXAMPLE 4
The experiment is carried out as in Example 2 with 200 ml of toluene as the solvent, 25 g of sodium, 50.33 g of Me2 SiCl2 (0.39 mol) and 22.64 g of freshly distilled (HMeClSi)2 NH (0.13 mol, 25 mol %). This gives 0.95 g of low-molecular products, 29.2 g of soluble copolymer (yield: 81.1%) and 2.15 g of insoluble solid.
EXAMPLE 5
The experiment is carried out as in Example 2 with 250 ml of toluene as the solvent, 28.73 g of sodium (1.25 g atoms), 50.33 g of Me2 SiCl2 (0.39 mol) and 36.6 g of (HMeClSi)2 NH (0.21 mol, 35 mol %). This gives 1.05 g of low-molecular products, 40.52 g of soluble copolymer (yield 91.3%) (viscous oil) and 0.95 g of insoluble copolymer
EXAMPLE 6
The experiment is carried out as in Example 2 with 150 ml of toluene, 19.55 g of sodium (0.85 g atom), 25.81 g of Me2 SiCl2 (0.2 mol) and 34.83 g of (HMeSiCl)2 NH (0.2 mol, 50 mol %). This gives 0.15 g of low-molecular products, 25.55 g of copolymer (soluble fluid oil) (yield: 79.2%) and 0.35 g of insoluble material.
EXAMPLE 7
The experiment is carried out as in Example 2 with 125 ml of toluene, 19.3 g of sodium (0.84 g atom, 5% excess), 34.5 g of methyldichlorosilane (0.3 mol) and 17.4 g of (ClMeHSi)2 NH (0.1 mol, 25 mol %). This gives 0.32 g of low-molecular products, 21.8 g of soluble copolymer (oil) (yield: 82.7%) and 1.5 g of insoluble copolymer.
EXAMPLE 8
The experiment is carried out as in Example 1 with 300 ml of a toluene/THF mixture in the respective proportions of 7 to 1 by weight, 32.2 g of sodium (1.4 g atoms), 79.94 g of freshly distilled dichloromethylvinylsilane (0.566 mol) and 17.42 g of (HMeClSi)2 NH (0.1 mol, 15 mol %). This gives 12.77 g of soluble copolymer (solid) (yield: 23%) and 41.4 g of insoluble solid copolymer (yield: 77%).
EXAMPLE 9
The experiment is carried out as in Example 2 with 250 ml of toluene, 23 g of sodium (1 g atom), 50.78 g of dichloromethylvinylsilane (0.36 mol) and 20.9 g of (HMeClSi)2 NH (0.12 mol, 25 mol %). This gives 17.95 g of soluble solid copolymer (yield: 43.4%) and 23.4 g of insoluble copolymer (56.6%).
EXAMPLE 10
The experiment is carried out as in Example 2 with 200 ml of toluene, 25.3 g of sodium (1.1 g atoms), 43.62 g of Me2 SiCl2 (0.338 mol, 65 mol %), 7.33 g of dichloromethylvinylsilane (0.052 mol, 10 mol %) and 22.64 g of (HMeClSi)2 NH (0.13 mol, 25 mol %). This gives 0.4 g of low-molecular products, 27.05 g of soluble copolymer (yield: 73.6%) in the form of fluid grease, and 8.8 g of insoluble solid copolymer.
EXAMPLE 11
The experiment is carried out as in Example 1 with 300 ml of toluene as the solvent, 21 g of sodium (0.91 g atom), 61.7 g of chlorinated disilanes of the empirical formula Me2.3 Si2 Cl3.7 and 26.1 g of (HMeClSi)2 NH (0 15 mol, 35 mol %). This gives 10.5 g of soluble copolymer (yield: 25.78%) and 23.3 g of insoluble copolymer (yield: 69.71%).
EXAMPLE 12
The experiment is carried out as in Example 2 with 125 ml of toluene, 16.1 g of sodium (0.7 g atom), 36.5 g of Me2 SiCl2 (0.28 mol) and 9.41 g of (HMeClSi)2 NMe (0.05 mol, 15 mol %). This gives 2.14 g of low-molecular products, 17.5 g of soluble copolymer (yield: 80.8%) and 3.27 g of insoluble solid.
Microanalysis of the soluble grease gives the following results: H (%): 9.65; N (%): 2.35; Cl (%): <0.2.
EXAMPLE 13
The experiment is carried out as in Example 2 with 125 ml of toluene, 16.1 g of sodium (0.7 g atom), 36.5 g of Me2 SiCl2 (0.28 mol) and 10.1 g of (EtHClSi)2 NH (0.05 mol, 15 mol %). This gives 1.07 g of low-molecular products, 16.98 g of soluble white grease (yield: 73.95%) and 2.62 g of insoluble solid.
Microanalysis of the soluble grease gives the following results H (%): 9.65; N (%): 3.42; Cl (%): 0.78.
EXAMPLE 14
The experiment is carried out as in Example 2 with 120 ml of toluene, 13.5 g of sodium (0.59 g atom), 27.1 g of Me2 SiCl2 (0.21 mol) and 20.9 g of (HPhClSi)2 NH (0.07 mol, 25 mol %). This gives 0.47 g of low-molecular products, 25.12 g of soluble copolymer (yield 89 3%) and 1.93 g of insoluble materials.
Microanalysis of the soluble grease gives the following results: H (%): 6.95; N (%): 4.33; Cl (%): 1.59.
EXAMPLE 15
The experiment is carried out as in Example 2 with 150 ml of toluene, 14.94 g of sodium (0.65 g atom), 48.74 g of PhMeSiCl2 (0.255 mol) and 7.84 g of (HMeClSi)2 NH (0.045 mol, 15 mol %). This gives 0.09 g of low-molecular products, 34.54 g of soluble copolymer (yield: 99.3%) and 0.15 g of insoluble solid.
EXAMPLE 16
The experiment is carried out as in Example 2 with 160 ml of toluene, 16.1 g of sodium (0.7 g atom), 45.87 g of PhMeSiCl2 (0.24 mol) and 13.93 g of (HMeClSi)2 NH (0.08 mol, 25 mol %). This gives 0.23 g of low-molecular products, 36.64 g of soluble copolymer and 0.13 g of insoluble materials.
EXAMPLE 17
The experiment is carried out as in Example 2 with 165 ml of toluene, 17.24 g of sodium (0.75 g atom), 37.3 g of Me2 SiCl2 (0.289 mol) and 10.11 g of (HViClSi)2 NH (0.051 mol, 15 mol %). This gives 0.46 g of low-molecular products, 7.06 g of soluble grease (yield: 30.3%) and 18.27 g of insoluble materials.
The heat treatment (thermolysis) of the copolymers according to the invention is described in the following Examples.
EXAMPLE 18
The equipment consists of a 500 ml long-necked silica round-bottomed flask provided with a thermometer sleeve, an inlet for inert gas (argon) and a water-cooled silica reflux condenser connected to a precision gas meter. The soluble copolymer prepared according to Example 1 is introduced into the flask under an inert atmosphere (13.95 g), it being possible for the material to be weighed in a glove box, and the equipment is then purged carefully with argon.
Thermolysis is effected by progressively heating the flask to a temperature of 500° C. by means of a fluidized sand bath. The operation is stopped after 5 h, at which point the temperature of the reactIon medIum has reached 433° C. and the total volume of gas evolved is 1725 cm3.
After subtraction of the dead volume of the equipment, the volume of gas is 104.6 cm3 /g, based on the mass of product used. The contents of the flask are taken up with 200 cm3 of hexane, after cooling, and stirred for one hour with a magnetic stirrer until optimum dissolution has been achieved.
After filtration in a glove box, an insoluble solid is obtained which weighs 3.7 g after the solvent has been removed under vacuum. The filtrate is concentrated on a Rotavapor and then devolatilized for 1 h at 250° C. under 1 mm of mercury. 0.82 g of low-molecular products is then collected, together with 4.63 g of solid polycarbosilazane with a softening point of 210° C. on a Koffler bench (yield relative to the copolymer used: 33.2%). Proportion of residue at 900° C.: 64%.
Microanalysis of the soluble copolymer gives the following results: N (%): 3.2; Cl (%): <0.25.
EXAMPLE 19
The experiment is carried out as in Example 18 using the copolymer prepared in Example 1 (13.95 g). Duration: 5 h. Temperature of the sand bath: 500° C. Final temperature of the reaction medium 413° C. Volume of gas (calculated as previously): 82.4 cm3 /g.
Microanalysis of the soluble copolymer gives the following results: N (%): 4.5; Cl (%): <0.18.
Balance:
Low-molecular products: 1.76 g
Soluble polycarbosilazane: 5.4 g (yield: 38.7%); Softening point: 190° C.; proportion of residue at 900° C.: 66%;
Insoluble polycarbosilazane: 2.45 g;
EXAMPLE 20
The experiment is carried out as described in Example 18 using 12.8 g of copolymer prepared according to Example 2. Duration: 3 h 45 min. Temperature of the sand bath: 450° C. Final temperature of the reaction medium: 402° C. ##EQU1##
Balance
Low-molecular products: 2.1 g
Soluble polycarbosilazane: 6.7 g (yield: 52.3%); N (%): 3.72; Cl (%): 0.38; Softening point on Koffler bench 250° C.; Proportion of residue: 66% at 1400° C.;
Insoluble polycarbosilazane: 0.45 g
EXAMPLE 21
The experiment is carried out as described in Example 18 starting with 12.8 g of copolymer prepared according to Example 2. Duration: 4 h 30 min. Temperature of the sand bath: 425° C. Final temperature of the reaction medium: 390° C. ##EQU2##
Balance
Low-molecular products: 1.5 g
Soluble polycarbosilazane: 7.5 g (yield: 58.6%); N (%): 5.36; Cl (%): 0.50; Softening point on Koffler bench: 170° C.;
Insoluble material: 0.1 g
EXAMPLE 22
The experiment was carried out as described in Example 18 with 11.45 g of copolymer prepared according to Example 3. Duration of thermolysis: 50 min. Temperature of the sand bath: 325° C. Final temperature of the reaction medium: 322° C. ##EQU3##
Balance
Low-molecular products: 1.4 g
Soluble polycarbosilazane: 4.2 g (yield: 36.7%); N (%): 3.88; Cl (%): 0.28; Softening point: 20° C.;
Insoluble material: 4 g
EXAMPLE 23
The experiment is carried out as described in Example 18 with 11.9 g of copolymer prepared according to Example 3. Duration of thermolysis: 4 h. Temperature of the sand bath: 275° C. Final temperature of the reaction medium: 273° C. ##EQU4##
Balance
Low-molecular products: 1.15 g
Soluble polycarbosilazane: 4.35 g (yield: 36.5%); N (%): 3.37; Cl (%): <0.01; Softening point: 50° C.;
Insoluble material: 4.9 g
EXAMPLE 24
The experiment is carried out as described in Example 18 with 13.8 g of copolymer prepared according to Example 4. Duration of thermolysis: 4 h 45 min. Temperature of the sand bath: 400° C. Final temperature of the reaction medium: 376° C. ##EQU5##
Balance
Low-molecular products: 1.7 g
Soluble polycarbosilazane: 7.9 g (yield: 57.2%); Softening point: above 250° C.;
Insoluble material: 0.1 g
Example 25
The experiment is carried out as described in Example 18 with 13.95 g of copolymer prepared according to Example 4. Duration of thermolysis: 3 h 10 min. Temperature of the sand bath: 400° C. Final temperature of the reaction medium 374° C. ##EQU6##
Balance
Low-molecular products 1 1 g
Soluble polycarbosilazane: 9.3 g (yield 66.7%); N (%): 4.62; Cl (%): 0.7; Softening point: 110° C.;
Insoluble material: 0.5 g
EXAMPLE 26
The experiment is carried out as described in Example 18 with 15 g of copolymer prepared according to Example 5. Duration of thermolysis: 4 h 30 min. Temperature of the sand bath: 400° C. Final temperature of the reaction medium 375° C. ##EQU7##
Balance
Low-molecular products: 0.6 g
Soluble polycarbosilazane 10.2 g (yield: 68%); Softening point: 135° C.;
Insoluble material: 0.1 g
EXAMPLE 27
The experiment is carried out as described in Example 18 starting with 15 g of copolymer prepared according to Example 5. DuratIon of thermolysis: 3 h min. Temperature of the sand bath: 400° C. Final temperature of the reaction medium: 373° C. ##EQU8##
Balance:
Low-molecular products 0 55 g
Soluble polycarbosilazane: 10 g (yield: 66.7%); Softening point: above 250° C.;
Insoluble material: 0.2 g
Pyrolysis at 1200° C., under argon, of the soluble polycarbosilazane of this Example gave 72% of residue. The ceramic thus obtained is totally amorphous according to the X-ray spectrum After heating to 1600° C., it appears to be formed of SiC and Si3 N4 microdomains according to photoelectron spectroscopy.
EXAMPLE 28
The experiment is carried out as described in Example 18 starting with 11 g of copolymer prepared according to Example 7. Duration of thermolysis: 5 h. Temperature of the sand bath: 350° C. Final temperature of the reaction medium: 328° C. ##EQU9##
Balance
Low-molecular products: 3.2 g
Soluble polycarbosilazane: 5.45 g (yield: 49.5%);
Softening point: 110° C.;
Insoluble material 0.5 g

Claims (9)

What is claimed is:
1. Copolymers containing --Si--N-- and --Si--Si-- bonds, and having in their main chains --Si--Si--N-- sequences, --Si--Si--n sequences, and --Si--(Si)n --Si--N-- sequences wherein n≧1, said copolymers being obtained by the polycondensation of
(a) at least one silane, at least one disilane, or a mixture of said disilanes; and silane having the formula RR1 SiCl2 ; and said disilane having the formula Clx SiMe3-x --SiMe3-y Cl7 in which 1≦x≦3 and 1≦y≦3; and
(b) at least one disilazane of the formula ##STR5## in which formulae: R2 is a halogen atom, and
R, R1 and R3, which are identical or different, are selected from the group consisting of a hydrogen atom, and alkyl, alkenyl, alkynyl, cycloalkyl, cycloalkenyl, aryl, alkylaryl, and alkenylaryl hydrocarbon radicals.
2. Copolymers according to claim 1 in which R2 =Cl, R=H and R1 =R3 =CH3.
3. Copolymers according to claim 1 in which the material designated as (a) is a chlorinated disalane or a mixture of chlorinated disilanes.
4. Polycarbosilazanes which are obtained by thermolysis of a copolymer according to claim 1, between 250° and 550° C. under a dry inert atmosphere.
5. Silicon carbonitrides which are obtained by heating a polycarbosilazane according to claim 4, to a temperature of 900° to 1000° C. under an inert atmosphere.
6. Copolymers according to claim 2 in which the material designated as (a) is a chlorinated disilane or a mixture of chlorinated disilanes.
7. Polycarbosilazanes which are obtained by thermolysis of a copolymer according to claim 2, between 250° and 550° C. under a dry inert atmosphere.
8. Silicon carbonitrides which are obtained by heating a polycarbosilazane according to claim 7 to a temperature of 900° to 1000° C. under an inert atmosphere
9. A copolymer according to claim 1 wherein R2 is Br or Cl.
US07/204,677 1987-06-10 1988-06-09 Copolymers containing si-n and si-si bonds, polycarbosilazanes obtained by pyrolysis of the said copolymers, and use of the said polycarbosilazanes for the preparation of silicon carbonitride Expired - Fee Related US4992523A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8708091A FR2616436B1 (en) 1987-06-10 1987-06-10 SI-N AND SI-SI BINDING COPOLYMERS, POLYCARBOSILAZANES OBTAINED BY PYROLYSIS OF SAID COPOLYMERS AND USE OF SAID POLYCARBOSILAZANES FOR THE PREPARATION OF SILICON CARBONITRIDE
FR8708091 1987-06-10

Publications (1)

Publication Number Publication Date
US4992523A true US4992523A (en) 1991-02-12

Family

ID=9351897

Family Applications (1)

Application Number Title Priority Date Filing Date
US07/204,677 Expired - Fee Related US4992523A (en) 1987-06-10 1988-06-09 Copolymers containing si-n and si-si bonds, polycarbosilazanes obtained by pyrolysis of the said copolymers, and use of the said polycarbosilazanes for the preparation of silicon carbonitride

Country Status (14)

Country Link
US (1) US4992523A (en)
EP (1) EP0296028A3 (en)
JP (1) JPS6454033A (en)
KR (1) KR890000561A (en)
CN (1) CN88103481A (en)
AU (1) AU604916B2 (en)
BR (1) BR8802892A (en)
DK (1) DK319588A (en)
FI (1) FI882621A (en)
FR (1) FR2616436B1 (en)
IL (1) IL86690A (en)
NO (1) NO882420L (en)
PT (1) PT87677B (en)
ZA (1) ZA884156B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5157096A (en) * 1989-07-18 1992-10-20 Shin-Etsu Chemical Co., Ltd. Method and apparatus for preparing organic silazane polymer and method for preparing inorganic fibers
US5187252A (en) * 1990-01-27 1993-02-16 Hoechst Aktiengesellschaft Silazane polymers containing sicl groups, process for their preparation, silicon nitride-containing ceramic materials which can be prepared from them, and their preparation
US5268496A (en) * 1992-05-27 1993-12-07 Wacker-Chemie Gmbh Process for the preparation of polysilazanes
US5494978A (en) * 1991-12-04 1996-02-27 Tonen Corporation Modified polysilazane and process for preparation thereof
US8680210B2 (en) 2011-05-02 2014-03-25 Bridgestone Corporation Method for making functionalized polymer

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2652081A1 (en) * 1989-09-21 1991-03-22 Rhone Poulenc Chimie PROCESS FOR PREPARING AN SI3N4-SIC COMPOSITE
FR2673201A1 (en) * 1991-02-26 1992-08-28 Rhone Poulenc Chimie Inorganic fibres based on silicon, carbon, nitrogen and oxygen
EP1967540B1 (en) * 2005-12-26 2013-04-03 Kaneka Corporation Curable composition
JP2020102525A (en) 2018-12-21 2020-07-02 メルク、パテント、ゲゼルシャフト、ミット、ベシュレンクテル、ハフツングMerck Patent GmbH Siliceous film-forming composition containing block copolymer, and manufacturing method of siliceous film using the same

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3853567A (en) * 1972-04-19 1974-12-10 Bayer Ag Production of shaped articles of homogeneous mixtures of silicon carbide and nitride
US3892583A (en) * 1972-09-05 1975-07-01 Bayer Ag Production of shaped articles of silicon carbide and silicon nitride
US4340619A (en) * 1981-01-15 1982-07-20 Dow Corning Corporation Process for the preparation of poly(disilyl)silazane polymers and the polymers therefrom
US4540803A (en) * 1983-11-28 1985-09-10 Dow Corning Corporation Hydrosilazane polymers from [R3 Si]2 NH and HSiCl3
EP0161751A1 (en) * 1984-03-12 1985-11-21 Dow Corning Corporation Process for the preparation of polymetallo(disily) silazane polymers and the polymers therefrom
US4612383A (en) * 1985-04-26 1986-09-16 S R I International Method of producing polysilazanes
EP0208972A2 (en) * 1985-07-11 1987-01-21 HÜLS AMERICA INC. (a Delaware corporation) Polysilane-siloxane oligomers and copolymers and methods of making the same
EP0212485A2 (en) * 1985-08-16 1987-03-04 Teijin Limited Process for producing shaped silicon carbide article from the same
US4656300A (en) * 1985-06-26 1987-04-07 Rhone Poulenc Specialites Chimiques Process for a thermal treatment of a polysilazane containing .tbd.SiH groups and .tbd.Si--NH-- groups
DE3717450A1 (en) * 1986-06-02 1987-12-03 Europ Propulsion New soluble copolymers of di:chloro-silane cpds.
US4745205A (en) * 1986-11-03 1988-05-17 Dow Corning Corporation Novel preceramic polymers derived from cyclic silazanes and halogenated disilanes and a method for their preparation
US4767831A (en) * 1985-06-24 1988-08-30 Dow Corning Corporation Process for preparing ceramic materials
US4800221A (en) * 1987-08-25 1989-01-24 Dow Corning Corporation Silicon carbide preceramic polymers

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2590584B1 (en) * 1985-11-28 1988-03-04 Rhone Poulenc Spec Chim PROCESS FOR THE PREPARATION, IN TWO STEPS, OF CROSS-LINKS OF ORGANOPOLYSILAZANES WITH IMPROVED THERMAL RESISTANCE, WHICH MAY BE USED IN PARTICULAR AS A CERAMIC PRECURSOR

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3853567A (en) * 1972-04-19 1974-12-10 Bayer Ag Production of shaped articles of homogeneous mixtures of silicon carbide and nitride
US3892583A (en) * 1972-09-05 1975-07-01 Bayer Ag Production of shaped articles of silicon carbide and silicon nitride
US4340619A (en) * 1981-01-15 1982-07-20 Dow Corning Corporation Process for the preparation of poly(disilyl)silazane polymers and the polymers therefrom
US4540803A (en) * 1983-11-28 1985-09-10 Dow Corning Corporation Hydrosilazane polymers from [R3 Si]2 NH and HSiCl3
EP0161751A1 (en) * 1984-03-12 1985-11-21 Dow Corning Corporation Process for the preparation of polymetallo(disily) silazane polymers and the polymers therefrom
US4612383A (en) * 1985-04-26 1986-09-16 S R I International Method of producing polysilazanes
US4767831A (en) * 1985-06-24 1988-08-30 Dow Corning Corporation Process for preparing ceramic materials
US4656300A (en) * 1985-06-26 1987-04-07 Rhone Poulenc Specialites Chimiques Process for a thermal treatment of a polysilazane containing .tbd.SiH groups and .tbd.Si--NH-- groups
EP0208972A2 (en) * 1985-07-11 1987-01-21 HÜLS AMERICA INC. (a Delaware corporation) Polysilane-siloxane oligomers and copolymers and methods of making the same
EP0212485A2 (en) * 1985-08-16 1987-03-04 Teijin Limited Process for producing shaped silicon carbide article from the same
DE3717450A1 (en) * 1986-06-02 1987-12-03 Europ Propulsion New soluble copolymers of di:chloro-silane cpds.
US4745205A (en) * 1986-11-03 1988-05-17 Dow Corning Corporation Novel preceramic polymers derived from cyclic silazanes and halogenated disilanes and a method for their preparation
US4800221A (en) * 1987-08-25 1989-01-24 Dow Corning Corporation Silicon carbide preceramic polymers

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5157096A (en) * 1989-07-18 1992-10-20 Shin-Etsu Chemical Co., Ltd. Method and apparatus for preparing organic silazane polymer and method for preparing inorganic fibers
US5187252A (en) * 1990-01-27 1993-02-16 Hoechst Aktiengesellschaft Silazane polymers containing sicl groups, process for their preparation, silicon nitride-containing ceramic materials which can be prepared from them, and their preparation
US5494978A (en) * 1991-12-04 1996-02-27 Tonen Corporation Modified polysilazane and process for preparation thereof
US5268496A (en) * 1992-05-27 1993-12-07 Wacker-Chemie Gmbh Process for the preparation of polysilazanes
US8680210B2 (en) 2011-05-02 2014-03-25 Bridgestone Corporation Method for making functionalized polymer

Also Published As

Publication number Publication date
EP0296028A2 (en) 1988-12-21
KR890000561A (en) 1989-03-15
FI882621A (en) 1988-12-11
PT87677B (en) 1992-10-30
JPS6454033A (en) 1989-03-01
NO882420D0 (en) 1988-06-02
AU604916B2 (en) 1991-01-03
BR8802892A (en) 1989-01-03
DK319588D0 (en) 1988-06-10
IL86690A0 (en) 1988-11-30
IL86690A (en) 1992-02-16
AU1761688A (en) 1988-12-15
ZA884156B (en) 1989-03-29
FI882621A0 (en) 1988-06-03
EP0296028A3 (en) 1989-03-08
FR2616436B1 (en) 1989-12-29
PT87677A (en) 1988-07-01
DK319588A (en) 1988-12-11
CN88103481A (en) 1988-12-28
FR2616436A1 (en) 1988-12-16
NO882420L (en) 1988-12-12

Similar Documents

Publication Publication Date Title
US4414403A (en) Branched polycarbosilanes and their use in the production of silicon carbide
CA1231515A (en) Preceramic organosilazane polymers
US4656300A (en) Process for a thermal treatment of a polysilazane containing .tbd.SiH groups and .tbd.Si--NH-- groups
US4472591A (en) Hydrosilyl-modified polycarbosilane precursors for silicon carbide
EP0123934B1 (en) Polysilane precursors containing olefinic groups for silicon carbide
US4992523A (en) Copolymers containing si-n and si-si bonds, polycarbosilazanes obtained by pyrolysis of the said copolymers, and use of the said polycarbosilazanes for the preparation of silicon carbonitride
US4550151A (en) Organoborosilicon polymer and a method for the preparation thereof
US5010158A (en) Process for preparing polysiloxazane compositions and the products formed thereby
CA1281477C (en) Method for converting si-h containing polysiloxanes to new and useful preceramic polymers and ceramic materials
JP2511074B2 (en) Pre-ceramic polymer, ceramic material and methods for producing the same
US4730026A (en) Cross-linked organosilazane polymers
US5138080A (en) Polysilamethylenosilanes and process for their preparation
CA1287432C (en) Preceramic polymers derived from cyclic silazanes and halogenated disilanes and a method for their preparation
US4497787A (en) Branched polycarbosilanes and their use in the production of silicon carbide
US5086126A (en) Method for producing functional silazane polymers
EP0052694B1 (en) Branched polycarbosilanes and their use in the production of silicon carbide
US5204434A (en) Polycarbosilanes and process for preparing them
US5250648A (en) Preparation of organic silizane polymers and ceramic materials therefrom
JPH0238127B2 (en)
US5182411A (en) Polymeric chlorosilazanes, process for their preparation, ceramic materials containing silicon nitride which can be manufactured therefrom, and their manufacture
US5100975A (en) Chlorine-containing silazane polymers, process for their preparation, ceramic material containing silicon nitride which can be prepared from them, and their preparation
US5196556A (en) Polysubstituted chlorine-containing silazane polymers, process for their preparation, ceramic materials containing silicon nitride which can be manufactured therefrom, and their manufacture
JPS6172026A (en) Production of polysilazane resin
US4608242A (en) Hydrosilyl-modified polycarbosilane precursors for silicon carbide
JPH05148366A (en) Preparation of silazane polymer and preparation of ceramic material from silazane polymer

Legal Events

Date Code Title Description
AS Assignment

Owner name: SOCIETE ANONYME: SOCIETE EUROPEENNE DE PROPULSION

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:BACQUE, ERIC;PILLOT, JEAN-PAUL;DUNOGUES, JACQUES;AND OTHERS;REEL/FRAME:004941/0402

Effective date: 19880711

Owner name: SOCIETE ANONYME: SOCIETE EUROPEENNE DE PROPULSION

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BACQUE, ERIC;PILLOT, JEAN-PAUL;DUNOGUES, JACQUES;AND OTHERS;REEL/FRAME:004941/0402

Effective date: 19880711

AS Assignment

Owner name: RHONE-POULENC CHIMIE, FRANCE

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:SOCIETE ANONYME: SOCIETE EUROPEENNE DE PROPULSION;REEL/FRAME:005450/0741

Effective date: 19900918

CC Certificate of correction
CC Certificate of correction
REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
FP Lapsed due to failure to pay maintenance fee

Effective date: 19950215

STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362